Low temperature decomposition of PCDD/PCDF, chlorobenzenes and PAHs by TiO2-based V2O5–WO3 catalysts

The oxidation of representative congeners of polychlorinated dibenzo-p-dioxins (PCDDs), polychlorinated dibenzofurans (PCDFs), polychlorinated chlorobenzenes (PCBzs), and of polyaromatic hydrocarbons (PAHs) was investigated on two commercial V2O5–WO3/TiO2-based catalysts, optimized for the combined reduction of nitrogen oxides and decomposition of dioxins. The non-chlorinated polyaromatic compounds (including non-chlorinated dibenzodioxin and dibenzofuran) are destroyed at temperatures as low as 150°C with an efficiency of more than 95%. PCDD and PCDF were also removed from the gas phase with an efficiency of >98%. However, at 150°C they remained mainly unchanged (up to 75%) adsorbed on the catalyst. A decrease in the oxidation rate with increasing chlorine substitution was found for the PCDD/PCDF. This could be explained by an increasing “redox potential” with increasing chlorine substitution due to the electron withdrawing effect of the chlorine. For the more volatile monoaromatic PCBz, however, the effect of lowering the volatility with increasing chlorine substitution (resulting in longer residence time on the catalyst) over-compensates the effect of the increasing “redox potential” with higher degree of chlorination.

[1]  S. Imamura,et al.  Decomposition of 1,2-dichloroethane on titanium dioxide/silica , 1989 .

[2]  M. Abraham,et al.  Low-temperature catalytic oxidation of 1,4-dichlorobenzene , 1991 .

[3]  V. Solinas,et al.  Microcalorimetric characterisation of acid–basic catalysts , 1998 .

[4]  P. Forzatti,et al.  Preparation and characterization of extruded monolithic ceramic catalysts , 1998 .

[5]  T. Mori,et al.  Catalytic decomposition of dioxin from MSW incinerator flue gas , 1996 .

[6]  J. Dumesic,et al.  Vanadia/Titania Catalysts for Selective Catalytic Reduction (SCR) of Nitric-Oxide by Ammonia: I. Combined Temperature-Programmed in-Situ FTIR and On-line Mass-Spectroscopy Studies , 1995 .

[7]  A. Wokaun,et al.  In Situ Diffuse Reflectance FTIR Study of the Selective Catalytic Reduction of NO by NH3 over Vanadia-Titania Aerogels , 1994 .

[8]  M. D. Amiridis,et al.  Catalytic oxidation of 1,2-dichlorobenzene over V2O5/TiO2-based catalysts , 1998 .

[9]  M. Kishida,et al.  Catalytic oxidative decomposition of chlorofluorocarbons (CFCs) in the presence of hydrocarbons , 1994 .

[10]  J. Ross,et al.  The development of supported vanadia catalysts for the combined catalytic removal of the oxides of nitrogen and of chlorinated hydrocarbons from flue gases , 1997 .

[11]  S. Chatterjee,et al.  Decomposition characteristics and reaction mechanisms of methylene chloride and carbon tetrachloride using metal-loaded zeolite catalysts , 1996 .

[12]  G. Schetter,et al.  Destruction of PCDD and PCDF in refuse incineration plants by primary and secondary measures , 1991 .

[13]  B. Rordorf Prediction of vapor pressures, boiling points and enthalpies of fusion for twenty-nine halogenated dibenzo-p-dioxins , 1987 .

[14]  G. Bond,et al.  Vanadium oxide monolayer catalysts Preparation, characterization and catalytic activity , 1991 .

[15]  P. Forzatti,et al.  Recent Advances in De‐NOxing Catalysis for Stationary Applications , 1996 .

[16]  R. Lago,et al.  Catalytic decomposition of chlorinated organics in air by copper chloride based catalysts , 1996 .

[17]  B. Rordorf Prediction of vapor pressures, boiling points and enthalpies of fusion for twenty-nine halogenated dibenzo-p-dioxins and fifty-five dibenzofurans by a vapor pressure correlation method , 1989 .